US1861415A - Treatment of electrodes - Google Patents
Treatment of electrodes Download PDFInfo
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- US1861415A US1861415A US540808A US54080831A US1861415A US 1861415 A US1861415 A US 1861415A US 540808 A US540808 A US 540808A US 54080831 A US54080831 A US 54080831A US 1861415 A US1861415 A US 1861415A
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- electrode
- oil
- electrodes
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- impregnated
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 43
- 238000000034 method Methods 0.000 description 30
- 229910052799 carbon Inorganic materials 0.000 description 23
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 22
- 239000003921 oil Substances 0.000 description 21
- 229910002804 graphite Inorganic materials 0.000 description 20
- 239000010439 graphite Substances 0.000 description 20
- 239000002383 tung oil Substances 0.000 description 20
- 230000008569 process Effects 0.000 description 18
- 239000000243 solution Substances 0.000 description 17
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 14
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 9
- 150000003839 salts Chemical class 0.000 description 9
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 8
- 239000000460 chlorine Substances 0.000 description 8
- 229910052801 chlorine Inorganic materials 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 6
- 230000009471 action Effects 0.000 description 6
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 6
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- VMPVEPPRYRXYNP-UHFFFAOYSA-I antimony(5+);pentachloride Chemical compound Cl[Sb](Cl)(Cl)(Cl)Cl VMPVEPPRYRXYNP-UHFFFAOYSA-I 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 description 5
- 239000011707 mineral Substances 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 238000005660 chlorination reaction Methods 0.000 description 4
- 230000000379 polymerizing effect Effects 0.000 description 4
- 229910021653 sulphate ion Inorganic materials 0.000 description 4
- 239000012267 brine Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 3
- 239000001993 wax Substances 0.000 description 3
- 229910001514 alkali metal chloride Inorganic materials 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 210000004243 sweat Anatomy 0.000 description 2
- 239000010913 used oil Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 229910001508 alkali metal halide Inorganic materials 0.000 description 1
- 150000008045 alkali metal halides Chemical class 0.000 description 1
- 229940075103 antimony Drugs 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- OHZZTXYKLXZFSZ-UHFFFAOYSA-I manganese(3+) 5,10,15-tris(1-methylpyridin-1-ium-4-yl)-20-(1-methylpyridin-4-ylidene)porphyrin-22-ide pentachloride Chemical compound [Cl-].[Cl-].[Cl-].[Cl-].[Cl-].[Mn+3].C1=CN(C)C=CC1=C1C(C=C2)=NC2=C(C=2C=C[N+](C)=CC=2)C([N-]2)=CC=C2C(C=2C=C[N+](C)=CC=2)=C(C=C2)N=C2C(C=2C=C[N+](C)=CC=2)=C2N=C1C=C2 OHZZTXYKLXZFSZ-UHFFFAOYSA-I 0.000 description 1
- TWXDDNPPQUTEOV-FVGYRXGTSA-N methamphetamine hydrochloride Chemical compound Cl.CN[C@@H](C)CC1=CC=CC=C1 TWXDDNPPQUTEOV-FVGYRXGTSA-N 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- XFZRQAZGUOTJCS-UHFFFAOYSA-N phosphoric acid;1,3,5-triazine-2,4,6-triamine Chemical compound OP(O)(O)=O.NC1=NC(N)=NC(N)=N1 XFZRQAZGUOTJCS-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- -1 salts ferric chloride Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/009—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
- C04B41/52—Multiple coating or impregnating multiple coating or impregnating with the same composition or with compositions only differing in the concentration of the constituents, is classified as single coating or impregnation
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/80—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone of only ceramics
- C04B41/81—Coating or impregnation
- C04B41/89—Coating or impregnation for obtaining at least two superposed coatings having different compositions
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/042—Electrodes formed of a single material
- C25B11/043—Carbon, e.g. diamond or graphene
- C25B11/044—Impregnation of carbon
Definitions
- This invention concerns an improved method for impregnating porous articles of carbon, graphite, graphitized carbon, or the like, for the purpose of prolongingthe useful' life or other characteristics thereof; and is particularly applicable to the preparation of such articles to resist chemical attack, such as occurs when the same are used as electrodes in the electrolysis of alkali metal halides or for parts of electrolytic cells, etc: where sub ject to oxidizing action.
- a carbon or graphite electrode when used in a process for electrolyzing alkali metal chloride solutions, tends to absorb the salt solution, chlorine and oxygen are liberated Within the voids of the electrode and as a result it becomes oxidized throughout and disintegrates.
- the present invention involves a further modification of the above described processes for treatment of carbon electrodes, but is an improvement over all known methods in that the product obtained by the herein described process consists of a carbon and/or graphite electrode which has not only been impregnated with Chinawood oil but which has been further treated in such a manner as to both chlorinate and polymerize (or coagulate) the so usedoil within the voids of the electrode.
- a carbon and/or graphite electrode is impregnated with Chinawood oil, then the so used oil simultaneously chlorinated and polymerized within said electrode by means of a chloride ion containing solution of a strong mineral acid and a olymerizing salt.
- Free chlorine is preferably. but not necessarily, present in the above mentioned mineral acid solution during treatment of the impregnated electrode therewith.
- Example 1 A graphitized carbon plate was placed in a suitable air tight container and the latter evacuated to an absolute pressure of approximately 110 millimeters. Chinawood oil was then admitted to the container and the pressure thereon brought to and maintained at 125 pounds gauge during a period of 5 hours. The-oil was then drained from the container and steam admitted thereto, in order to facilitate draining of excess oil adhering to the plate. (The oil content of a plate, at this point, is generally found to be approximately 9 to 12 per cent of the original weight of the latter, which means that I approximately 5080 per cent of the original voids in the plate are filled with oil).
- the container containing the graphite plate was again evacuated to an absolute pressure of approximatelyllO millimeters and maintained at that pressure for about 2 minutes. then air admitted.
- the plate was removed from its container and plunged, while hot. into a solution of ferric chloride in hydrochloric acid where it was permitted to cool to room temperature, then removed and dried. The plate was then ready for use as an electrode in the previously mentioned electrolytic process.
- Example 2 A graphitized carbon plate was treated in a way similar to that described in Example 1, except that chlorine was passed through the solution of ferric chloride in hydrochloric acid during the time the impregnated plate was immersed and cooling therein. It was found, upon analysis ofvarious' cuts from cross-sections both of this plate and of the plate described in Example 1, that in the present example the polymerized oil was chlorinated at a greater depth from the surface of the electrode and more uniformly than it was in the product obtained according to the method described in Example 1.
- Electrodes prepared according to our method. have beenlfound to be impervious to penetration by brine and to be very resistant to further action by the chlorine liberated during the aforementioned electrolytic process. Tests made indicate that they have a longer active life than do such electrodes treated by any previously described process.
- carbon and/or raphite shall be used to characterize an e ectrode or article composed chiefly of carbon, graphite, or graphitized carbon.
- a method of treating a carbon and/0r graphite electrode the steps which consist in mpregnating said electrode with Chinawood oil, heating the impregnated electrode with steam, then cooling said electrode in a hydrochloric acid solution containing at least Zine of the following group of salts :ferric graphite electrode, the steps which consist in treating such an electrode,-impregnated with Chinawood oil, with steam, then cooling said electrode in a hydrochloric acid solution containing free chlorine and also containing at least one of the following group of salts ferric chloride, ferric sulphate, ferricnitrate, a gimony pentachloride, titanium tetrachlor1 e.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Structural Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Metallurgy (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Carbon And Carbon Compounds (AREA)
- Ceramic Products (AREA)
Description
A Patented May 31, 1 932 UNITED STATES PATENT-L OFFICE 'f RALBH M. HUNTER, LEROY C. STEWART, HOWARD E. HOUSER, AND LEE DE PBEE, OI MIDLAND, MICHIGAN, ASSIGNORS TO THE DOW CHEMICAL COMPANY, OI MIDLAND, MICHIGAN, A CORPORATION ,OF MICHIGAN I N0 Drawing.
This invention concerns an improved method for impregnating porous articles of carbon, graphite, graphitized carbon, or the like, for the purpose of prolongingthe useful' life or other characteristics thereof; and is particularly applicable to the preparation of such articles to resist chemical attack, such as occurs when the same are used as electrodes in the electrolysis of alkali metal halides or for parts of electrolytic cells, etc: where sub ject to oxidizing action.
A carbon or graphite electrode, when used in a process for electrolyzing alkali metal chloride solutions, tends to absorb the salt solution, chlorine and oxygen are liberated Within the voids of the electrode and as a result it becomes oxidized throughout and disintegrates. In order to prevent such action, it is general practice to impregnate the electrodes with oils, waxes or the like prior to using them in the aforementioned process. Such treatment increases theefi'iciency of the electrolytic process and materially lengthens the life of the-electrodes themselves. While paraflin oil and waxes are generally used for impregnating electrodes, it has been found that better results are obtained when Chinawood oil and similar drying oils are substituted therefor.
Although treatment of electrodes, in the manner described above,.decreases the diffusion of brine through the same and in general improves their quality, certain disadvantages result from such practice." During use of the so treated electrodes in the process for electrolyzing alkali metal chlorides, for instance, the oil with which they are impregn ated becomes partially chlorinated and tends to swell, with the result that the electrodes sweat oil and at the same time crumble or wear away. The oil or wax so lib erated from the electrodes 'proves further disadvantageous in that it tends to foul and obstruct the cell diaphragm, thereby interfering with the conduct ofthe'process as a whole. However. after an electrode impregnated in the described manner has been larges, 1y worn away, the portion thereof'remaining is found to be hard; it no longer sweats oil; it is impervious to bririe; and further TREATMENT or ELECTRODES Application filed May 28, 1931. Serial no. smsos.
oxidation and distintegration of said remnant electrode proceeds with extreme slowness. This change in character of the electrode is believed to result from the oil remaining therein having become as completeso thereafter absent. It is therefore desirable 00 I I to change the character of impregnated elec-:
trodes to that last described before using the same.
An improved process for impregnatingcarbon electrodes, described by O. A. Laubi 05 w in United States Patent 1,779,242, consists in impregnating such electrodes with ch10: rinated hydrocarbons before using the same in electrolytic cells. By such treatment, further chlorination of the hydrocarbon oils (0 in a co-pending application of R. M. Hunter 15 and L. E. Ward, Serial No. 461,632, filed June 16, 1930. Briefly, their process consists in first impregnating carbon or graphite electrodes with a drying oil, e. g. Chinawood oil, then subjecting the impregnated'electrodes to the action of chlorine over a con,- siderable period of time. Although an electrode treated in such a manner often has an active life which exceeds that of one impreg-i nated with Chinawood oil but not prechlorinated by as much as 50 per cent, the process is still disadvantageous in that the chlorination step proceeds slowly, generally requiring aperiod of several weeksor even months for appreciable chlorination of the impregnating oil to be effected. Furthermore, chlorination occurs most readily at the surface of the electrode and is liable to be non-uniform in depth of penetration- Therefore, electrodes treated in such a manner are not consistent in quality. In another co-pending ap 1ication of R. M. Hunter and L. E; Ward, erial No. 513.049, filed February 2, 1931, and entitled Process for treating electrodes, a process is described whereby carbon or graphite electrodes are impregnated with a prechlorinated drying oil such as Chinawood oil. Such treatment has been found to pro duce a product, uniform in quality, and superior in durability'to electrodes prepared by the other mentioned processes.
' The present invention involves a further modification of the above described processes for treatment of carbon electrodes, but is an improvement over all known methods in that the product obtained by the herein described process consists of a carbon and/or graphite electrode which has not only been impregnated with Chinawood oil but which has been further treated in such a manner as to both chlorinate and polymerize (or coagulate) the so usedoil within the voids of the electrode. We havefound that a carbon and/or graphite electrode, impregnated with Chinawood oil, when treated with a chloride ion containing solution of a strong mineral acid and at least one of the followin group of salts :-.ferric chloride, ferric sul ate, ferric nitrate, antimony pentachloride and titanium tetrachloride, is acted upon in such a manner that the oil therein is both polymerized and partially chlorinated, the result being that the electrode is rendered impervious to penetration by brine and very resistant to further action by chlorine. The present invention, then, consists of a process, and of the product from said process, hereinafter fully described and articularly pointedout in the claims, where,-
y a carbon and/or graphite electrode is impregnated with Chinawood oil, then the so used oil simultaneously chlorinated and polymerized within said electrode by means of a chloride ion containing solution of a strong mineral acid and a olymerizing salt. Free chlorine is preferably. but not necessarily, present in the above mentioned mineral acid solution during treatment of the impregnated electrode therewith. V
Preliminary to the treatment of electrodes in the manner hereinafter described, tests were made to determine the effect of hydrochloric acid solutions of various salts upon Chinawood oil. Into a test tube were placed 10 cubic centimeters of a solution consisting of 50 per cent Chinawood oil and 50 per cent kerosene, by weight. To this solution were added 0.1 gram of ferric chloride, 0.5 gram of concentrated (37 per cent) hydrochloric acid and 0.5 gram of water. The mixture was thoroughly agitated, then permitted to stand at room temperature. In approximately 20 minutes the Chinawood oil was polymerized toa solid mass. The liquid remaining after such treatment was found to contain ferrous chloride, and analysis of the polymerized product proved it to have been partially chlorinated. By means of similar tests it was found that a similar chlorinated and polymerized product could be obtained by using ferric nitrate, ferric sulfate, or antimony pentachloride instead of the aforementioned ferric chloride. It was also found that titanium tetrachloride would produce the above described polymer, if used in a concentrated form.
' Several of the various ways of applying the principle of our invention are described in the following examples. It is to be understood, however, that such examples are purely illustrative and are not to be construed as a limitation on the invention.
Example 1 A graphitized carbon plate was placed in a suitable air tight container and the latter evacuated to an absolute pressure of approximately 110 millimeters. Chinawood oil was then admitted to the container and the pressure thereon brought to and maintained at 125 pounds gauge during a period of 5 hours. The-oil was then drained from the container and steam admitted thereto, in order to facilitate draining of excess oil adhering to the plate. (The oil content of a plate, at this point, is generally found to be approximately 9 to 12 per cent of the original weight of the latter, which means that I approximately 5080 per cent of the original voids in the plate are filled with oil). After treatment .with steam, the container containing the graphite plate was again evacuated to an absolute pressure of approximatelyllO millimeters and maintained at that pressure for about 2 minutes. then air admitted. The plate was removed from its container and plunged, while hot. into a solution of ferric chloride in hydrochloric acid where it was permitted to cool to room temperature, then removed and dried. The plate was then ready for use as an electrode in the previously mentioned electrolytic process.
Example 2 A graphitized carbon plate was treated in a way similar to that described in Example 1, except that chlorine was passed through the solution of ferric chloride in hydrochloric acid during the time the impregnated plate was immersed and cooling therein. It was found, upon analysis ofvarious' cuts from cross-sections both of this plate and of the plate described in Example 1, that in the present example the polymerized oil was chlorinated at a greater depth from the surface of the electrode and more uniformly than it was in the product obtained according to the method described in Example 1.
-Electrodes, prepared according to our method. have beenlfound to be impervious to penetration by brine and to be very resistant to further action by the chlorine liberated during the aforementioned electrolytic process. Tests made indicate that they have a longer active life than do such electrodes treated by any previously described process.
In the claims it shallbe' understood that the term carbon and/or raphite shall be used to characterize an e ectrode or article composed chiefly of carbon, graphite, or graphitized carbon.
Other forms of applying'theprinciple of our invention may be employed instead of the ones here explained, change being made in the method or composition, provided the steps or 5 ingredients stated by any of the following claims or the equivalent of such stated steps or ingredients be employed.
We therefore particularly point out and distinctly claim as our invention 1. In a method of treating a carbon and/or graphite article, the steps which consist in impregnating said article with Chinawood oil and then simultaneously chlorinating and polymerizing said oil by means of a chloride ion containing solution of a strong mineral acid and a polymerizing salt.
2. In a method of treating a carbon and/or graphite electrodeAshe steps which consist in impregnating said electrode with Chinawood oil, then further subjecting the thus impregnated electrode to the action of a hydrochloric acid solution containing at least one of the following group of salts :-ferric chloride,'ferric sulphate, ferric nitrate, anti- -mony pentachloride, titanium tetrachloride.
3. In a method of treating a carbon and/or graphite electrode, the steps which consist in impregnating said electrode with Chinawood oil, heating the impregnated electrode with steam,'then cooling. said electrode in a hydrochloric acid solution containing free chlorine and also containing at least one of I the following group of salts :f'erric chloride, ferric sulphate, ferric nitrate, antimony pentachloride, titanium tetrachloride. 4. In a method of treating a carbon and/0r graphite electrode, the steps which consist in mpregnating said electrode with Chinawood oil, heating the impregnated electrode with steam, then cooling said electrode in a hydrochloric acid solution containing at least Zine of the following group of salts :ferric graphite electrode, the steps which consist in treating such an electrode,-impregnated with Chinawood oil, with steam, then cooling said electrode in a hydrochloric acid solution containing free chlorine and also containing at least one of the following group of salts ferric chloride, ferric sulphate, ferricnitrate, a gimony pentachloride, titanium tetrachlor1 e. i
8. In a method of treating a carbon and/0r graphite electrode, the steps which consist in treating such an'electrode, impregnated with Chinawood oil, with steam, then cooling said electrode in a hydrochloric acid solution containing at least one of the following group of and/or graphite electrode, the steps which consist in impregnating said electrode with Chinawood oil, then treating the so impregnated electrode with steam, and finally coo ing the electrode in a hydrochloric acid solution containing ferric chloride.
11. As a product of manufacture, a carbon and/or graphite article impregnated with a polymerized form of Chinawood oil which is at least in part chlorinated.
12. As a product of manufacture, a carbon and/or graphite electrode impregnated with a polymerized form of Chinawood oil which is at east in part chlorinated.
Signed by us this 23rd day of May 1931. RALPH M. HUNTER.
LEROY C. STEWART. HOWARD E. HOUSER. LEE DE FREE, I
chloride, ferric sul hate, ferric nitrate, antimony pentachlori e, titanium tetrachloride.
5. In a method of treating a carbon and/or graphite electrode, wood oil, the step which consists in simultaneously chlorinating and polymerizing said oil by means of a chloride ion containing soluton of a strong mineral acid and a polymerizing salt.
reg'nated. with China- I I 6. In a meth 'od of treating a carbon and/or' graphite electrodedhe step which consists i3 ate Sub ecting such an electrode; impre with chinawood oilfto the action a hydrochloric acid solution containing at leg'st one of the'following group of salts :e-ferric chloride, ferric sulphate, ferric nitrate, antimony pentachloride, titanium tetrachloride.
7. a method of treating a carbon and/or
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US540808A US1861415A (en) | 1931-05-28 | 1931-05-28 | Treatment of electrodes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US540808A US1861415A (en) | 1931-05-28 | 1931-05-28 | Treatment of electrodes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1861415A true US1861415A (en) | 1932-05-31 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US540808A Expired - Lifetime US1861415A (en) | 1931-05-28 | 1931-05-28 | Treatment of electrodes |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1861415A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2418420A (en) * | 1943-02-08 | 1947-04-01 | Westinghouse Electric Corp | Process for impregnating carbon brushes |
| US2433212A (en) * | 1942-10-09 | 1947-12-23 | Ici Ltd | Electrode for use in electrolytic cells |
| US2500209A (en) * | 1946-07-11 | 1950-03-14 | Great Lakes Carbon Corp | Production of shaped carbon articles |
| US2820728A (en) * | 1955-06-21 | 1958-01-21 | Diamond Alkali Co | Method of treating carbon electrodes with polymerizable oil |
| US2920004A (en) * | 1958-02-20 | 1960-01-05 | Columbia Southern Chem Corp | Method of treating drying oil impregnated graphite electrode |
| US3057794A (en) * | 1961-10-10 | 1962-10-09 | Pittsburgh Plate Glass Co | Electrolytic cell diaphragm |
-
1931
- 1931-05-28 US US540808A patent/US1861415A/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2433212A (en) * | 1942-10-09 | 1947-12-23 | Ici Ltd | Electrode for use in electrolytic cells |
| US2418420A (en) * | 1943-02-08 | 1947-04-01 | Westinghouse Electric Corp | Process for impregnating carbon brushes |
| US2500209A (en) * | 1946-07-11 | 1950-03-14 | Great Lakes Carbon Corp | Production of shaped carbon articles |
| US2820728A (en) * | 1955-06-21 | 1958-01-21 | Diamond Alkali Co | Method of treating carbon electrodes with polymerizable oil |
| US2920004A (en) * | 1958-02-20 | 1960-01-05 | Columbia Southern Chem Corp | Method of treating drying oil impregnated graphite electrode |
| US3057794A (en) * | 1961-10-10 | 1962-10-09 | Pittsburgh Plate Glass Co | Electrolytic cell diaphragm |
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